Low-bacteria milk powders with a high wpni (iii)

ABSTRACT

A low-bacteria milk powder with a high WPNI is suggested, which is obtainable by
     (a) providing a raw milk;   (b) heating the raw milk in at least one tubular heat exchanger to a temperature of at least 20° C.;   (c) separating the cream, obtaining a skimmed milk;   (d) pasteurising the skimmed milk in a tubular heat exchanger for a period from 10 to 60 seconds at a temperature from 72 to 75° C.;   (e) evaporating the pasteurised skimmed milk to a dry matter content from 35 to 55% by weight; and   (f) drying the pasteurised skimmed milk concentrate in a spray tower.

FIELD OF THE INVENTION

The invention is in the field of dairy products and relates to a processfor the production of spray-dried milk powders which are characterisedby exhibiting both a reduced bacterial contamination and a high WPNI.

STATE OF THE ART

For the production of low-bacteria milk powders, for example, alreadypasteurised skimmed milk with a dry matter content of about 9% isevaporated to a concentration of about 40%. However, the concentratesstill contain a large quantity of heat-resistant bacteria and spores,which particularly originates from the maize silage fed to the cows, andwhich ends up in the raw milk as a result of insufficient stablehygiene. For this reason, it has been required to this date to subjectthe concentrates to high temperature treatment before spraying, by meansof which the bacteria and spores are quantitatively destroyed, and as aresult of which a bacteria-free and high-quality product is obtained.

However, high temperature treatment does not only have an effect on thebacteria and spores, also the valuable whey proteins are denatured,either completely or to a very large extent, thus adversely changing theproduct in its functionality and nutritional physiology. Whey proteinsare in albumins and globulins; they particularly includealpha-lactalbumin and beta-lactoglobulin, serum albumin, proteosepeptone and the immunoglobulins. From a nutritional perspective, wheyproteins are high-value milk constituents, which are specifically usedto build muscle, for example, in protein supplements. While untreatedskimmed milk has a so-called whey protein nitrogen index (WPNI) of above6, specifically of 6.1, as a parameter for its whey protein content,this value falls below 1 during regular ultra-high temperaturetreatment, which is extremely undesired.

An alternative for this might consist in performing the temperaturetreatment at lower temperatures, for example, at about 70° C. instead ofmore than 100° C. In fact, products such obtained have a WPNI of above5, however, the bacterial contamination is so high that products areobtained which are, at best, difficult to market.

In this context, it is referred to CN 2011 1116530 A1, which discloses aprocess for the production of low temperature milk powder, in theprocess of which skimmed milk is subjected to microfiltration at between40 to 50° C., and filtered through an inorganic membrane with a poresize from 0.8 to 1.4 μm. Subsequently, the microfiltration product issterilised at between 72 and 78° C. and concentrated at between 45 and75° C. in a falling film evaporator. This is followed by spray drying,in the process of which the temperature at the inlet is between 180 and200° C., and between 80 and 105° C. at the outlet. The document neitherspecifies the WPNI of the resulting products, nor does it contain anyinformation on the bacterial contamination thereof.

EP 2679098 A1 (DMK) also discloses a process for the production oflow-bacteria milk powders, wherein a microfiltration step is used toseparate the bacteria; this application, however, does not contain anyreference on the production of powders enriched with active agents.

While filtration processes as a process step in dairy processing arevery suitable for at least significantly reducing the bacterialcontamination, this is a technically complex and thus costly measurewhich is not likely to be realised in the context of low sales pricesfor dairy products.

Therefore, the production of milk powders usually comprises thefollowing steps: The raw milk is heated to 55° C. in a combined heatexchanger/separator, initially in a plate heat exchanger(PWT—Plattenwärmetauscher), and then the cream is separated. The skimmedmilk is heated in an evaporator, is then pasteurised in a tubular heatexchanger (RWT—Röhrenwärmetauscher) (72-75° C., 15-45 s) and cooled downin a further PWT to 8° C. From this point, it is heated to more than 70°C. in the next PWT and is then concentrated. In order to operate theconcentrator in continuous mode, the milk is introduced into a buffertank and introduced into the concentrator from this point. Theconcentrated milk leaves the concentrator at a temperature of about 40°C., is re-heated to 70° C., and spray-dried at 200° C. The powder leavesthe tower at a temperature of about 30° C.

This conventional mode of operation, however, entails a number ofdisadvantages:

-   1. In plate heat exchangers, thermophilic bacteria find optimum    growth conditions at about 55° C. Also the intermediate re-heating    leads to a strong growth of bacteria.-   2. Whey proteins—particularly when present in non-concentrated    milk—do not tolerate any temperatures exceeding 70° C. which are,    however, required to kill the bacteria. Therefore, the resulting    powders have a WPNI of 6.2 maximum.-   3. The powders made in the tower have more than 1,000 thermophilic    and more than 5,000 mesophilic bacteria, which is still admissible,    but which should be reduced.

The object of the present invention was therefore to provide asimplified process for the production of powders made in the tower onthe basis of skimmed milk, wherein the powders should exhibit a lowerbacteria count and a higher WPNI at the same time.

DESCRIPTION OF THE INVENTION

A first subject-matter of the invention relates to a low-bacteria milkpowder with a high WPNI, which is obtainable by

-   (a) providing a raw milk;-   (b) heating the raw milk to a temperature of at least 20° C. in at    least one tubular heat exchanger;-   (c) separating the cream, obtaining a skimmed milk;-   (d) pasteurising the skimmed milk in a tubular heat exchanger for a    period from 10 to 60 seconds at a temperature from 72 to 75° C.;-   (e) evaporating the pasteurised skimmed milk to a dry matter content    from 35 to 55% by weight; and-   (f) drying the pasteurised skimmed milk concentrate in a spray    tower.

Preferably, the milk powder according to the invention contains lessthan 1,000 thermophilic and/or less than 5,000 mesophilic bacteriaand/or no pathogenic bacteria, and is characterised by a WPNI of atleast 6, preferably from 7.0 to 7.5. In doing so, the object ofproviding a qualitatively improved product described above has not onlybeen completely fulfilled, this task has also been solved in asignificantly less technically complex way.

BRIEF DESCRIPTION OF THE DRAWING

The present invention will be described in greater detail with referenceto the accompanying drawing which is a flow chart illustrating themethod according to the present invention.

Process

A further subject-matter of the invention relates to a process for theproduction of a low-bacteria milk powder with a high WPNI, comprisingthe following steps:

-   (a) providing a raw milk;-   (b) heating the raw milk to a temperature of at least 20° C. in at    least one tubular heat exchanger;-   (c) separating the cream, obtaining a skimmed milk;-   (d) pasteurising the skimmed milk in a tubular heat exchanger for a    period from 10 to 60 seconds at a temperature from 72 to 75° C.;-   (e) evaporating the pasteurised skimmed milk to a dry matter content    from about 35 to about 55% by weight.-   (f) drying the pasteurised skimmed milk concentrate in a spray    tower.

Preferably, milk powders are produced by the process according to theinvention that contain less than 1,000 thermophilic and/or less than5,000 mesophilic bacteria and/or no pathogenic bacteria, characterisedby a WPNI of at least 6, preferably from 7.0 to 7.5.

Separation

Separation (steps b and c) is understood as being the separation of thecream up to a fat content of about 0.5% by weight, and the removal ofsolids. The process is performed under hot conditions at a temperaturein the range from about 50 to about 60° C., or under cold conditions ata temperature from about 15 to about 35° C.

In the process according to the invention it may be advantageous toperform the separation cold. In doing so, it is advantageous if thetemperature of the cold condition of the raw milk is adjusted to a valuethat is optimal for separation by means of heat exchange using a heatcarrier medium. Usually, the raw milk is available in a cooledcondition, the temperature of which does not correspond to the valuewhere cold separation can be performed most effectively and most gentlywith respect to the milk fat (cream). It is, therefore, adapted to thevalue that is optimal for separation by means of heat exchange. Theexchanged cold temperature from the process may be made available toother processes that are carried out in a dairy, particularly by aso-called heat exchanger. For example, the temperature of the cooled rawmilk does not exceed 6° C., while the optimum temperature for coldseparation is in the range of about 20° C. In this case, heat exchangeis performed by heating the raw milk, so that the temperature of thecold condition thereof is increased to a value within this range. Indairies there usually is excess heat. Therefore, low temperature waterobtained in dairy processes can be used as a heat carrier medium forheating. Said low temperature water is supplied to the heat exchangeprocess at a temperature which is, for example, in the range of 40° C.,and is then cooled down by heat exchange to a temperature which is, forexample, in the range of 25° C. In doing so, the process of theinvention provides an important cold source for dairy processes.

Within the present invention, tubular heat exchangers are employedinstead of plate heat exchangers which are commonly used otherwise.Surprisingly, this measure leads to the fact that the growth ofthermophilic bacteria is significantly reduced, even at otherwiseoptimum conditions at 55° C. In doing so, it has proved to beparticularly advantageous to perform the heating of the raw milk in step(b) in two serially connected heat exchangers, of which at least onerepresents a tubular heat exchanger, wherein the milk in the firstexchanger is heated to about 35° C., and to 55° C. in the second one.

The separation of solids and the skimming of a fat content of about 4%by weight is usually carried out in a downstream component, preferably aseparator. Said components are adequately known from the state of theart. Separators of the company GEA Westfalia Separator GmbH, which allowthe joint or single separation of solids(http://www.westfalia-separator.com/de/anwendungen/molkereitechnik/milch-molke.html),are widely used in the dairy industry. Preferred cold milk separatorsare marketed by the manufacturer under the name “Procool”. Correspondingcomponents have also been disclosed, for example, in DE 10036085 C1 andDE 10361526 B3 (Westfalia) and are perfectly known to one skilled in theart. Therefore, no explanations are needed on how to carry out theseprocess steps.

Pasteurisation

This process step (d) is a legal measure intended to ensure that themilk may be considered microbiologically safe and be approved forconsumption. Pasteurisation is preferably performed in heat exchangers,and also herein tubular heat exchangers have again proved to beparticularly suitable. There is a temperature gradient at the heatexchangers, which, however, is selected such that the product is heatedto a temperature from about 70 to 80° C. and particularly from about 72to 75° C. for a residence time of a minimum of 10 and a maximum of 60seconds, preferably about 30 seconds.

Concentration

The pasteurised milk leaves the tubular heat exchanger, optionally afterpassing a device for keeping food warm at a temperature of about 40° C.This is followed by a step in which the pasteurised skimmed milk isdehydrated and concentrated to a dry matter content from about 30 toabout 55% by weight, and particularly from about 35 to about 45% byweight. Conventional evaporators are particularly suitable for this.However, there had been a prejudice up to the date of application thatan evaporator may only be reliably operated in continuous mode if it issupplied with a similarly continuous stream of milk. In other words, ifthe quantity of milk coming from the pasteurisation steposcillates—which may always be the case in large plants—the evaporatorwill operate irregularly. For this reason, plant developers have alwaysprovided that the milk is initially pumped into a feed tank (“buffertank”) either after the milk has left the separator or after it haspassed the pasteurisation step; from this tank it is then, in fact,possible to continuously supply the milk into the evaporator. However,this measure is particularly disadvantageous, because storage is eitherperformed at comparably low temperatures in the range of about 55° C. sothat the temperature difference compared with the evaporator is not toolarge, or it is performed at the approximately same temperature as inthe evaporator, i.e. at about 75° C. In the first case, the wheyproteins are saved, but there are ideal conditions for the growth ofthermophilic bacteria; in the second case, a large part of the valuableproteins is denatured, in addition—which has not been known to this dateeither—a rapid growth of bacteria is still taking place also at 70° C.,as can be taken from the following Table 1:

TABLE 1 Growth of thermophilic bacteria as a function of time andtemperature Temperature [° C.] Time [h] Bacteria count/ml 65 1 2,300 210,100 3 830,000 4 1,290,000 5 2,540,000 70 1 1,900 2 4,100 3 510,000 4340,000 5 1,700,000 75 1 300 2 100 3 200 4 <100 5 <100 80 1 100 2 100 3100 4 100 5 100In addition, also the damage of the whey proteins caused by temperatureproves to be significantly more serious than had been known to thisdate, as is shown by the course of the WPNI of a pasteurised skimmedmilk stored at 74° C. according to Table 2:

TABLE 2 Growth of thermophilic bacteria as a function of time andtemperature (74° C.) Time [s] WPNI-preparation 1 WPNI-preparation 2 307.62 7.18 300 7.38 6.90 600 5.94 6.86 900 5.76 5.61 1,200 5.60 5.031,500 5.40 4.38 1,800 4.62 4.19 2,100 4.37 3.89 2,400 4.29 3.83 2,7004.20 3.09

The applicant therefore decided to dispense with the interposition of afeed tank, originally planning to take into account that the evaporatormight exhibit operational disturbances; however, this has surprisinglyproved to be a technical prejudice, as modern evaporators can tolerateoscillations of the quantity used without causing any problems. Thisfinding was the key for being able to produce milk powders which arealso characterised by an improved quality in a more simple way.Accordingly, the particular findings of the invention include the factthat milk is not temporarily stored between the individual processsteps.

Further water-soluble additives and adjuvants may be added to theskimmed milk, either before or, preferably, after evaporation.

Drying

In the following process step, the skimmed milk concentrate is dried.Spray drying is preferably used here, with the temperature in the inlettypically ranging from about 180 to about 260° C., preferably, about220° C., and from about 80 to about 105° C. at the outlet. The milkconcentrate can be pre-heated to about 75° C., preferably, however, itis not heated any further before entering the spray tower; this alsoensures that there is neither a growth of bacteria nor a denaturationprocess. Alternatively, the products may also be dehydrated by beltdrying, freeze drying and the like.

Further additives in powder form may be added to the product before, butpreferably after spraying such as, for example, lactoferrin, lecithins,vitamins or food emulsifiers [EP 1314367 A1, NESTLE] and the like.

INDUSTRIAL APPLICATION

A further subject-matter of the invention relates to the use of the milkpowder of the invention for human nutrition.

EXAMPLES Comparison Example 1

Comparison example V1 relates to a common continuous process for theproduction of a skimmed milk powder which is sprayed via a tower.

To this end, raw milk is directed over a plate heat exchanger and heatedto 55° C.; in the connected separator the separation of the cream isperformed, as a result of which a skimmed milk is obtained. This milk isheated to a temperature of between 72 and 75° C. in a combination of twoplate heat exchangers, and is left there for about 30 seconds. The milksuch pasteurised is cooled down to about 8° C. to prevent the growth ofthermophilic bacteria, and is re-heated to 70° C. directly beforeconcentration, in the process of which the sequence of heating andcooling is essentially performed by heat exchange so that the loss ofenergy, in sum, is low. The heated milk is supplied to a collectiontank, from which the evaporator is continuously supplied. At thismoment, the concentrate with a dry matter content of about 55% by weighthas a WPNI of 6.5. The concentrate leaves the evaporator at atemperature of below 40° C. and enters a further plate heat exchanger inwhich it is heated to above 70° C. This entails a decrease of the WPNIto 6.2. The pre-heated concentrate is sprayed at 200° C. and leaves thetower at a temperature of 30° C., after passing further heat exchangers.The powder has a residual moisture of less than 5% by weight and a WPNIof between 6.0 and 6.2. Microbiological analysis shows that between1,000 and 5,000 thermophilic bacteria and between 5,000 and 10,000mesophilic bacteria are still present. On this basis, the powder can beclassified as suitable for human nutrition.

Example 1

Example 1 of the invention shows how not only the technical complexitycan be reduced and the WPNI can be increased, reducing the bacteriacount in a skimmed milk powder at the same time even though certainprocess steps are omitted.

To this end, raw milk is heated in two steps in a combination of a firstplate heat exchanger and a second tubular heat exchanger, initially to35° C., followed by 55° C., and the cream is separated by a processknown per se. The skimmed milk such obtained is pasteurised at 72 to 75°C. for a period of about 30 seconds in a further tubular heat exchangerwithout any further temperature treatment and without being temporarilystored, and is then introduced into the evaporator in a buffer tank,also without being temporarily stored. The concentrate with a dry mattercontent of about 55% by weight leaves the concentrator at a temperatureof about 40° C., having a WPNI of 7.5. Without any further heating, itis directly applied to the tower and sprayed at 200° C. A powder with aresidual moisture of less than 5% by weight is obtained, having a WPNIfrom 7.3 to 7.5. Microbiological analysis shows that the number of thethermophilic bacteria is below 1,000, and also the number of themesophilic bacteria is below 5,000.

Comparison Example V2

Example 1 was repeated; a buffer tank was interposed downstream of theseparator and upstream of the heater, in which the milk was stored at55° C. to ensure that the evaporator was continuously supplied withproduct. The powder obtained after spraying did have a WPNI of 7.3,however, it contained between 1,000 and 5,000 thermophilic bacteria andbetween 5,000 and 10,000 mesophilic bacteria.

Comparison Example V3

Example 1 was repeated; a buffer tank was interposed directly upstreamof the heater, in which the milk was stored at 74° C. to ensure that theevaporator was continuously supplied with product. The powder obtainedafter spraying did contain less than 1,000 thermophilic bacteria andabout 5,000 mesophilic bacteria, however, only a WPNI of 6.4 wasachieved.

These examples and comparison examples show that the employment oftubular heat exchangers is advantageous in comparison with plate heatexchangers. This also helps overcome the prejudice that continuousevaporation is only possible when the milk is stored in a buffer tank.

Example 1 is further explained in a flow chart (FIG. 1). Theabbreviations have the following meanings:

T=temperature treatmentRWT=tubular heat exchangerSEP=separatorPAST=pasteurisationCONC=evaporatorST=spray towerThe first RWT may also be replaced by a plate heat exchanger.The concentration step may be followed by a heating step in a heatexchanger of up to 75° C. if required.

1. A low-bacteria milk powder with a high whey protein nitrogen index,obtainable by (a) providing a raw milk; (b) heating the raw milk in atleast one tubular heat exchanger to a temperature of at least 20° C.;(c) separating the cream, obtaining a skimmed milk; (d) pasteurising theskimmed milk in a tubular heat exchanger for a period from 10 to 60seconds at a temperature from 72 to 75° C.; (e) evaporating thepasteurised skimmed milk to a dry matter content from 35 to 55% byweight; and (f) drying the pasteurised skimmed milk concentrate in aspray tower.
 2. The milk powder of claim 1, containing less than 1,000thermophilic bacteria per mg. and/or less than 5,000 mesophilic bacteriaper mg. and/or no pathogenic bacteria.
 3. The milk powder of claim 1,having a whey protein nitrogen index of at least
 6. 4. The milk powderof claim 3, having a whey protein nitrogen index of between 7.0 and 7.5.5. A process for the production of a low-bacteria milk powder with ahigh whey protein nitrogen index, comprising the following steps: (a)providing a raw milk; (b) heating the raw milk to a temperature of atleast 55° C. in at least one tubular heat exchanger; (c) separating thecream, obtaining a skimmed milk; (d) pasteurising the skimmed milk in atubular heat exchanger for a period from 10 to 60 seconds at atemperature from 72 to 75° C.; (e) evaporating the pasteurised skimmedmilk to a dry matter content from about 35 to about 55% by weight; and(f) drying the pasteurised skimmed milk concentrate in a spray tower. 6.The process of claim 5, wherein said milk powder has less than 1,000thermophilic bacteria per mg. and/or less than 5,000 mesophilic bacteriaper mg. and/or no pathogenic bacteria are produced.
 7. The process ofclaim 5, wherein said milk powder having a whey protein nitrogen indexof at least 6 is produced.
 8. The process of claim 7, wherein said milkpowder having a whey protein nitrogen index of between 7.0 and 7.5 isproduced.
 9. The process of claim 5, wherein heating the raw milk instep (b) is performed in two serially connected heat exchangers, wherebythe milk is heated to about 35° C. in the first exchanger and to about55° C. in the second exchanger.
 10. The process of claim 5, furthercomprising the step of adding water-soluble additives and adjuvants tothe milk either before or after evaporating.
 11. The process of claim 5,wherein the milk concentrate is directly sprayed, optionally without anyfurther heating.
 12. The process of claim 5, wherein spray drying isperformed at a temperature in the range from about 180 to about 260° C.13. The process of claim 5, further comprising the step of addingadditives and adjuvants in powder form to the milk after evaporating.14. The process of claim 5, wherein the milk is not stored during theindividual process steps.
 15. (canceled)